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Nomenclature Roman letters a A A b Ba c c cκ cp cs cv C C CD Cij CL Cp Cpmin d dj do D D Dm Ds Amplitude of wave-like disturbance Cross-sectional area or cloud radius Attenuation Power law index Bagnold number, ρS D2 γ̇/µL Concentration Speed of sound Phase velocity for wavenumber κ Specific heat at constant pressure Specific heat of solid or liquid Specific heat at constant volume Compliance Damping coefficient Drag coefficient Drag and lift coefficient matrix Lift coefficient Coefficient of pressure Minimum coefficient of pressure Diameter Jet diameter Hopper opening diameter Particle, droplet or bubble diameter Mass diffusivity Volume (or mass) mean diameter Sauter mean diameter 11 D(T ) D e E f f fL , fV Fi Fr F g gL , gV GN i GN h h H H He Hm i, j, k, m, n i I I ji jN i jN k k k kL , kV K K∗ Kc Kij Kn , Ks Kn K Determinant of the transfer matrix [T ] Thermal diffusivity Specific internal energy Rate of exchange of energy per unit volume Frequency in Hz Friction factor Liquid and vapor thermodynamic quantities Force vector Froude number Interactive force per unit volume Acceleration due to gravity Liquid and vapor thermodynamic quantities Mass flux of component N in direction i Mass flux of component N Specific enthalpy Height Height Total head, pT /ρg Henry’s law constant Haberman-Morton number, normally gµ4 /ρS 3 Indices Square root of −1 Acoustic impulse Rate of transfer of mass per unit volume Total volumetric flux in direction i Volumetric flux of component N in direction i Volumetric flux of component N Polytropic constant Thermal conductivity Boltzmann’s constant Liquid and vapor quantities Constant Cavitation compliance Keulegan-Carpenter number Added mass coefficient matrix Elastic spring constants in normal and tangential directions Knudsen number, λ/2R Frictional constants Typical dimension 12 t L L m ṁ mG mp M M∗ Mij M Ma n ṅ ni N (R), N (D), N(v) N∗ Nu p pT pa pG ps P Pe Pr q qi Q Q Q r, ri rd R R∗k RB Re Re R Turbulent length scale Inertance Latent heat of vaporization Mass Mass flow rate Mass of gas in bubble Mass of particle Mach number Mass flow gain factor Added mass matrix Molecular weight Martinelli parameter Number of particles per unit volume Number of events per unit time Unit vector in the i direction Particle size distribution functions Number of sites per unit area Nusselt number Pressure Total pressure Radiated acoustic pressure Partial pressure of gas Sound pressure level Perimeter Peclet number, usually W R/αC Prandtl number, ρνcp/k General variable Heat flux vector General variable Rate of heat transfer or release per unit mass Rate of heat addition per unit length of pipe Radial coordinate and position vector Impeller discharge radius Bubble, particle or droplet radius Resistance of component, k 1 Equivalent volumetric radius, (3τ /4π) 3 Equilibrium radius Reynolds number, usually 2W R/νC Gas constant 13 s s s S SD St Str t tc tu tT T T Tij ui uN i ur , uθ us u∗ U, Ui U∞ v V, Vi V V V̇ w W, Wi W∞ Wp Wt We W x, y, z xi x X z Coordinate measured along a streamline or pipe centerline Laplace transform variable Specific entropy Surface tension Surface of the disperse phase Stokes number Strouhal number Time Binary collision time Relaxation time for particle velocity Relaxation time for particle temperature Temperature Granular temperature Transfer matrix Velocity vector Velocity of component N in direction i Velocity components in polar coordinates Shock velocity Friction velocity Fluid velocity and velocity vector in absence of particle Velocity of upstream uniform flow Volume of particle, droplet or bubble Absolute velocity and velocity vector of particle Volume Control volume Volume flow rate Dimensionless relative velocity, W/W∞ Relative velocity of particle and relative velocity vector Terminal velocity of particle Typical phase separation velocity Typical phase mixing velocity Weber number, 2ρW 2 R/S Rate of work done per unit mass Cartesian coordinates Position vector Mass fraction Mass quality Coordinate measured vertically upward 14 Greek letters α β γ γ̇ Γ δ δd δm δT δ2 δij ζ η θ θ θw κ κ κL , κG λ λ λ Λ µ µ∗ ν ν ξ ρ σ σi σij D σij Σ(T ) Volume fraction Volume quality Ratio of specific heats of gas Shear rate Rate of dissipation of energy per unit volume Boundary layer thickness Damping coefficient Fractional mass Thermal boundary layer thickness Momentum thickness of the boundary layer Kronecker delta: δij = 1 for i = j; δij = 0 for i = j Fractional volume Coefficient of restitution Rate of dissipation of energy per unit mass Attenuation or amplification rate Bubble population per unit liquid volume Angular coordinate or direction of velocity vector Reduced frequency Hopper opening half-angle Wavenumber Bulk modulus of compressibility Shape constants Wavelength Mean free path Kolmogorov length scale Integral length scale of the turbulence Dynamic viscosity Coulomb friction coefficient Kinematic viscosity Mass-based stoichiometric coefficient Particle loading Density Cavitation number Inception cavitation number Stress tensor Deviatoric stress tensor Thermodynamic parameter 15 τ τi τn τs τw ψ ψ φ φ φ φ2L , φ2G , φ2L0 ϕ ω ωa ωi ωn ωm ωm ωp Ω Kolmogorov time scale Interfacial shear stress Normal stress Shear stress Wall shear stress Stokes stream function Head coefficient, ∆pT /ρΩ2 rd2 Velocity potential Internal friction angle Flow coefficient, j/Ωrd Martinelli pressure gradient ratios Fractional perturbation in bubble radius Radian frequency Acoustic mode frequency Instability frequency Natural frequency Cloud natural frequencies Manometer frequency Peak frequency Rotating frequency (radians/sec) Subscripts On any variable, Q: Qo Q1 , Q2 , Q3 Q1 , Q2 Q∞ Q∗ QA Qb QB QB QC Qc QD Initial value, upstream value or reservoir value Components of Q in three Cartesian directions Values upstream and downstream of a component or flow structure Value far from the particle or bubble Throat values Pertaining to a general phase or component, A Pertaining to the bulk Pertaining to a general phase or component, B Value in the bubble Pertaining to the continuous phase or component, C Critical values and values at the critical point Pertaining to the disperse phase or component, D 16 Qe Qe QG Qi Qij QL Qm QN QO Qr Qs QS QV Qw Qθ Equilibrium value or value on the saturated liquid/vapor line Effective value or exit value Pertaining to the gas phase or component Components of vector Q Components of tensor Q Pertaining to the liquid phase or component Maximum value of Q Pertaining to a general phase or component, N Pertaining to the oxidant Component in the r direction A surface, system or shock value Pertaining to the solid particles Pertaining to the vapor phase or component Value at the wall Component in the θ direction Superscripts and other qualifiers On any variable, Q: Q , Q, Q∗ Q̄ Q̀ Q̃ Q̇ Q̈ Q̂(s) Q̆ δQ Re{Q} Im{Q} Used to differentiate quantities similar to Q Mean value of Q or complex conjugate of Q Small perturbation in Q Complex amplitude of oscillating Q Time derivative of Q Second time derivative of Q Laplace transform of Q(t) Coordinate with origin at image point Small change in Q Real part of Q Imaginary part of Q 17 NOTES Notation The reader is referred to section 1.1.3 for a more complete description of the multiphase flow notation employed in this book. Note also that a few symbols that are only used locally in the text have been omitted from the above lists. Units In most of this book, the emphasis is placed on the nondimensional parameters that govern the phenomenon being discussed. However, there are also circumstances in which we shall utilize dimensional thermodynamic and transport properties. In such cases the International System of Units will be employed using the basic units of mass (kg), length (m), time (s), and absolute temperature (K). 18